CN115069053A - Tail gas and dust separation filter - Google Patents
Tail gas and dust separation filter Download PDFInfo
- Publication number
- CN115069053A CN115069053A CN202210880816.2A CN202210880816A CN115069053A CN 115069053 A CN115069053 A CN 115069053A CN 202210880816 A CN202210880816 A CN 202210880816A CN 115069053 A CN115069053 A CN 115069053A
- Authority
- CN
- China
- Prior art keywords
- gear
- ash
- box
- gas
- rotating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000000428 dust Substances 0.000 title claims abstract description 155
- 238000000926 separation method Methods 0.000 title claims abstract description 57
- 238000009413 insulation Methods 0.000 claims abstract description 82
- 238000004321 preservation Methods 0.000 claims abstract description 38
- 239000007787 solid Substances 0.000 claims abstract description 19
- 230000000670 limiting effect Effects 0.000 claims description 24
- 230000005291 magnetic effect Effects 0.000 claims description 20
- 230000005540 biological transmission Effects 0.000 claims description 7
- 230000007246 mechanism Effects 0.000 claims description 7
- 238000007789 sealing Methods 0.000 claims description 7
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 claims description 3
- 239000003302 ferromagnetic material Substances 0.000 claims description 3
- 239000000835 fiber Substances 0.000 claims description 3
- 239000012774 insulation material Substances 0.000 claims description 3
- 206010066054 Dysmorphism Diseases 0.000 claims 3
- 230000005389 magnetism Effects 0.000 claims 2
- 230000000694 effects Effects 0.000 claims 1
- 230000017525 heat dissipation Effects 0.000 claims 1
- 238000004140 cleaning Methods 0.000 abstract description 80
- 230000033001 locomotion Effects 0.000 abstract description 18
- 239000007789 gas Substances 0.000 description 138
- 230000009471 action Effects 0.000 description 44
- 239000002918 waste heat Substances 0.000 description 24
- 238000010586 diagram Methods 0.000 description 11
- 239000000779 smoke Substances 0.000 description 11
- 230000003068 static effect Effects 0.000 description 11
- 230000005484 gravity Effects 0.000 description 9
- 230000001133 acceleration Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 230000000903 blocking effect Effects 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000011084 recovery Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 230000009969 flowable effect Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000012824 chemical production Methods 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/28—Particle separators, e.g. dust precipitators, using filter brushes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto
- B08B9/08—Cleaning containers, e.g. tanks
- B08B9/087—Cleaning containers, e.g. tanks by methods involving the use of tools, e.g. brushes, scrapers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/10—Arrangements for using waste heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/10—Arrangements for using waste heat
- F27D17/15—Arrangements for using waste heat using boilers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D17/00—Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
- F27D17/20—Arrangements for treatment or cleaning of waste gases
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
本发明公开了一种尾气粉尘分离过滤器,包括保温组件、自旋转固气单向分离装置、立壁清灰装置和膛压滑变式自控组件和底座;所述膛压滑变式自控组件设于底座上,所述保温组件设于膛压滑变式自控组件上,所述自旋转固气单向分离装置设于保温组件内,所述立壁清灰装置活动设于保温组件内,所述立壁清灰装置位于自旋转固气单向分离装置上方,所述自旋转固气单向分离装置和立壁清灰装置设有若干组。本发明属于除尘设备技术领域,具体是指一种能够实现无动力往复运动、自清洁、从气体中分离固态粉尘的尾气粉尘分离过滤器。
The invention discloses a tail gas dust separation filter, comprising a heat preservation component, a self-rotating solid-gas one-way separation device, a vertical wall ash cleaning device, a chamber pressure sliding type automatic control component and a base; the chamber pressure sliding type automatic control component is provided with On the base, the thermal insulation component is arranged on the chamber pressure sliding type automatic control component, the self-rotating solid-gas one-way separation device is arranged in the thermal insulation component, the vertical wall dust cleaning device is movably arranged in the thermal insulation component, and the The vertical wall ash cleaning device is located above the self-rotating solid-gas one-way separation device, and the self-rotating solid-gas one-way separation device and the vertical wall ash cleaning device are provided with several groups. The invention belongs to the technical field of dust removal equipment, in particular to a tail gas dust separation filter capable of realizing unpowered reciprocating motion, self-cleaning, and separating solid dust from gas.
Description
技术领域technical field
本发明涉及除尘设备技术领域,具体涉及一种尾气粉尘分离过滤器。The invention relates to the technical field of dust removal equipment, in particular to a tail gas dust separation filter.
背景技术Background technique
余热锅炉是利用各种工业过程中的废气、废料或废液中的显热或(和)其可燃物质燃烧后产生的热量的锅炉,或在燃油(或燃气)的联合循环机组中,利用从燃气轮机排出的高温尾气热量的锅炉,广泛用于工业炉窑、动力机械和化工生产过程,但是高温含尘废气通过余热锅炉后,除温度降低外,还会沉降一部分尘粒,可能对设备造成堵塞和腐蚀,影响设备的使用寿命;为了加强环境保护和避免能源浪费,炉气要经过滤装置除尘后再进行排放或加以回收利用,在此过程中通常会用到预除尘装置,将弥散的粉尘颗粒从高温尾气分离出来。The waste heat boiler is a boiler that utilizes the sensible heat in the waste gas, waste or waste liquid in various industrial processes or (and) the heat generated by the combustion of its combustible substances, or in the combined cycle unit of fuel oil (or gas), using from Boilers with high-temperature exhaust heat from gas turbines are widely used in industrial furnaces, power machinery and chemical production processes. However, after high-temperature dust-laden exhaust gas passes through the waste heat boiler, in addition to the temperature reduction, some dust particles will settle, which may cause blockage of equipment. and corrosion, which will affect the service life of the equipment; in order to strengthen environmental protection and avoid energy waste, the furnace gas must be dedusted by a filter device before being discharged or recycled. In this process, a pre-dust device is usually used to remove the dispersed dust The particles are separated from the high temperature exhaust gas.
现有的预除尘装置中:重力沉降除尘装置只适用于净化密度大、粒径粗的粉尘;惯性除尘装置结构简单,阻力较小(10-80毫米水柱),但净化效率较低(40-80%);利用布袋除尘虽然效率高,但由于布袋的可耐受温度最高瞬间值仅有280℃,因此为了满足过滤器的需要,前端需要增加庞大的表冷器或者机力风冷器,在上述热交换过程中,温度下降的同时,热能也大量损失,从而造成直接的经济损失。Among the existing pre-dust removal devices: the gravity sedimentation dedusting device is only suitable for purifying dust with high density and coarse particle size; the inertial dedusting device has a simple structure and low resistance (10-80 mm water column), but the purification efficiency is low (40-80 mm water column). 80%); although the use of bag dust removal is highly efficient, since the maximum instantaneous temperature of the cloth bag is only 280°C, in order to meet the needs of the filter, a huge surface cooler or mechanical air cooler needs to be added at the front end. During the above heat exchange process, while the temperature drops, a large amount of heat energy is also lost, resulting in direct economic losses.
发明内容SUMMARY OF THE INVENTION
针对上述情况,为克服现有技术的缺陷,本发明提供了一种尾气粉尘分离过滤器,针对现有技术中存在的问题,利用尾气本身高速的特点,将尾气的动能转化为阻力交变器的动能,实现了无动力往复式移动清洁,同时利用尾气高压的特点,将尾气的压力转化为炉灰箱的压力,使尾气往复对炉灰箱与尾气箱进行循环冲压放压,驱动膛压控制滑块往复运动,实现炉灰箱中的灰尘不断被高压喷出;同时,通过毛刷一对气体可流动管径和固体可流动管径进行调节,实现对于气体低阻力、对于固体高阻力的设计,使过滤器中的烟尘被减速从气体中分离。In view of the above situation, in order to overcome the defects of the prior art, the present invention provides a tail gas dust separation filter. In view of the problems in the prior art, the kinetic energy of the tail gas is converted into a resistance alternator by utilizing the high-speed feature of the tail gas itself. At the same time, using the characteristics of high pressure of the exhaust gas, the pressure of the exhaust gas is converted into the pressure of the ash box, so that the exhaust gas reciprocates the ash box and the exhaust box to cyclically press and release the pressure and drive the chamber pressure. The reciprocating motion of the slider is controlled, so that the dust in the ash box is continuously ejected by high pressure; at the same time, a pair of gas flowable pipe diameters and solid flowable pipe diameters are adjusted by brushes to achieve low resistance to gas and high resistance to solids The design allows the soot in the filter to be decelerated and separated from the gas.
本发明采取的技术方案如下:本发明提供的一种尾气粉尘分离过滤器,包括保温组件、自旋转固气单向分离装置、立壁清灰装置和膛压滑变式自控组件和底座;所述膛压滑变式自控组件设于底座上,底座对膛压滑变式自控组件进行支撑固定,所述保温组件设于膛压滑变式自控组件上,所述自旋转固气单向分离装置设于保温组件内,保温组件对自旋转固气单向分离装置进行支撑固定,所述立壁清灰装置活动设于保温组件内,所述立壁清灰装置位于自旋转固气单向分离装置上方,所述自旋转固气单向分离装置和立壁清灰装置设有若干组,在尾气的带动下立壁清灰装置不断上下运动,对保温组件立壁上的灰尘进行清理;所述保温组件内设有限位架,所述限位架设有若干组,所述限位架之间设有限位杆,所述限位杆呈竖直方向设置,所述自旋转固气单向分离装置包括管壁一、转动扇、中轴、毛刷一和密封轴承,所述管壁一设于保温组件内,保温组件对管壁一进行支撑固定,所述毛刷一的一端设于管壁一内壁,所述毛刷一的另一端设有绒毛,所述毛刷一的一端为光杆设置,所述毛刷一设有若干组,若干组所述毛刷一组合为毛刷圆筒,所述密封轴承的外圈设于限位架上,所述中轴设于密封轴承的内圈上,限位架对密封轴承和中轴进行支撑固定,在外力的带动下中轴和密封轴承内圈做同轴转动,所述转动扇设于中轴上,所述转动扇设有若干组,所述转动扇倾斜设置,所述中轴上设有上支架和下支架,所述上支架的一端和下支架的一端设于中轴上,所述上支架的另一端和下支架的另一端设有除尘板,所述除尘板设有若干组,所述除尘板活动设于毛刷一中,所述除尘板倾斜设置,当锅炉的尾气通过保温组件流经自旋转固气单向分离装置时,尾气将驱动转动扇转动,转动扇带动中轴、上支架、下支架和除尘板做同心转动,由于转动扇倾斜的设于中轴上,原本竖直方向流动的气体遇到转动扇时将对转动扇产生一个水平方向的分力,推动转动扇旋转,由于力的作用是相互的,转动扇将给气体施加一个水平方向的反作用力,转动扇通过对气体施加的水平方向的反作用力推动粉尘飞入毛刷一中,除尘板和转动扇做同心转动且除尘板伸入毛刷一中,除尘板拍打毛刷一,使毛刷一上的粉尘在除尘板和惯性力的作用下运动到毛刷一的一端,毛刷一的另一端的绒毛部分阻挡了高速气流的通过,毛刷一的一端与管壁一组成了一个对于固体粉尘无阻力的下沉通道,且在毛刷一的另一端的绒毛中气体的密度小、体积小,尾气中的气体能够通过绒毛自由流动并上升,而粉尘作为固体颗粒密度大、体积大,在通过绒毛时阻力更大难以运动,在绒毛中流动的气体不再有足够的流速带动粉尘继续运动,粉尘被除尘板拍进毛刷一的一端内,在重力的作用下不断下降堆积,实现了对于气体低阻力、对于固体高阻力的设计,并在气体流动过程中除尘的功能。The technical scheme adopted by the present invention is as follows: a kind of exhaust dust separation filter provided by the present invention includes a heat preservation component, a self-rotating solid-gas one-way separation device, a vertical wall dust cleaning device, a chamber pressure sliding type automatic control component and a base; the The chamber pressure sliding automatic control assembly is arranged on the base, the base supports and fixes the chamber pressure sliding automatic control assembly, the heat preservation assembly is arranged on the chamber pressure sliding automatic control assembly, and the self-rotating solid-gas one-way separation device It is arranged in the thermal insulation component, and the thermal insulation component supports and fixes the self-rotating solid-gas one-way separation device. The vertical wall ash cleaning device is movably arranged in the thermal insulation component, and the vertical wall ash cleaning device is located above the self-rotating solid-gas one-way separation device. The self-rotating solid-gas one-way separation device and the vertical wall ash cleaning device are provided with several groups, and the vertical wall ash cleaning device continuously moves up and down driven by the exhaust gas to clean the dust on the vertical wall of the thermal insulation component; A limit frame, the limit frame is provided with several groups, a limit rod is arranged between the limit frames, the limit rod is arranged in a vertical direction, and the self-rotating solid-gas one-way separation device includes a pipe wall. , a rotating fan, a central shaft, a
其中,所述立壁清灰装置包括阻力交变器、支撑杆、管壁二和毛刷二,所述阻力交变器中间设有贯穿孔一,所述限位杆通过贯穿孔一贯穿阻力交变器设置,在外力的作用下阻力交变器可沿限位杆上下滑动,所述阻力交变器包括顶盘、旋转叶、转动盘、固定盘和传动机构,所述固定盘和限位杆滑动连接,所述固定盘上设有限位凸点,所述限位杆上设有滑动槽一,滑动槽一内表面光滑设置,所述限位凸点卡入滑动槽一中,当固定盘沿限位杆上下滑动时,一方面限位杆使固定盘只能沿竖直方向运动,另一方面限位杆使固定盘在沿竖直方向运动时不会发生转动;所述固定盘上设有固定螺栓、固定柱和外齿,所述转动盘活动设于固定盘上,所述转动盘上设有滑动槽二,所述滑动槽二贯穿转动盘设置,所述转动盘上设有内齿,所述固定螺栓和固定柱设于滑动槽二内,当转动盘受到外力作用时,滑动槽二可沿固定螺栓滑动,固定螺栓和固定柱对滑动槽二的移动起到限位作用,所述外齿与内齿相对设置,内齿与外齿组成一个带有内部轮齿的凹槽,所述固定螺栓上表面与转动盘上表面齐平,所述固定柱上表面高于转动盘上表面,所述顶盘设于固定柱上,固定柱对顶盘进行支撑固定;所述传动机构包括转动轴二、转动轴三、动力轮、第一齿轮、第二齿轮、牙盘、第三齿轮、第四齿轮、第五齿轮、第六齿轮和第七齿轮,所述固定盘设有缺口,所述转动轴二、转动轴三设于缺口侧壁上,缺口对转动轴二和转动轴三进行支撑和固定,所述动力轮活动设于转动轴二上,当阻力交变器沿限位杆上下移动时,动力轮在限位杆表面滚动,动力轮与限位杆之间竖直方向的作用力为静摩擦力,在外力的作用下动力轮可绕转动轴二转动,所述牙盘活动设于转动轴三上,在外力的作用下牙盘可绕转动轴三转动,所述第一齿轮设于动力轮上,所述第二齿轮设于牙盘上,所述第一齿轮与第二齿轮相互啮合,所述第三齿轮、第四齿轮、第五齿轮和第七齿轮活动设于固定盘上,所述第三齿轮与牙盘相互啮合,所述第四齿轮与第三齿轮相互啮合,所述第五齿轮为不完全齿轮,所述第五齿轮与外齿相啮合,第五齿轮在活动范围内只能和外齿相互啮合,不能与内齿啮合,所述第七齿轮与内齿和外齿相互啮合,所述第六齿轮设于第五齿轮上,所述第六齿轮与第四齿轮啮合,所述旋转叶设于第七齿轮上,旋转叶随第七齿轮的转动而转动,初始时,立壁清灰装置位于保温组件底部,旋转叶处于张开状态,当通入尾气后,由于旋转叶对气流的阻力大,气流对立壁清灰装置向上的力大于立壁清灰装置受到的向下的力,立壁清灰装置在气流的作用下将沿限位杆向上做加速运动,在立壁清灰装置的带动下动力轮沿限位杆顺时针向上滚动,并带动第一齿轮顺时针转动,第一齿轮带动第二齿轮和牙盘做逆时针转动,牙盘带动第三齿轮做顺时针转动,第三齿轮带动第四齿轮逆时针转动,第四齿轮带动第六齿轮和第五齿轮顺时针转动,第五齿轮带动外齿顺时针转动,外齿带动转动盘绕限位杆做顺时针转动,同时外齿带动第七齿轮在顺时针自传的同时沿内齿做顺时针公转,在第七齿轮的带动下旋转叶逐渐闭合,阻力交变器受到向上的力逐渐变小,并最终小于向下的力,立壁清灰装置向上运动的速度变化由向上加速变为向上减速,在立壁清灰装置向上运动的速度降为0m/s之前,立壁清灰装置与保温组件上方的限位架接触,在限位架的阻挡下立壁清灰装置速度变为0m/s,此时旋转叶已经完全收回到阻力交变器中,随后立壁清灰装置在重力的作用下向下加速运动,在立壁清灰装置的带动下动力轮沿限位杆逆时针滚动,并带动第一齿轮逆时针转动,第一齿轮带动第二齿轮和牙盘做顺时针转动,牙盘带动第三齿轮做逆时针转动,第三齿轮带动第四齿轮顺时针转动,第四齿轮带动第六齿轮和第五齿轮逆时针转动,第五齿轮带动外齿逆时针转动,外齿带动转动盘绕限位杆做逆时针转动,同时外齿带动第七齿轮在顺时针自传的同时沿内齿做逆时针公转,在第七齿轮的带动下旋转叶逐渐张开,阻力交变器受到向上的力逐渐变大,并最终大于向下的力,立壁清灰装置向下运动的速度变化由向下加速变为向下减速,在立壁清灰装置向下运动的速度降为0m/s之前,立壁清灰装置与保温组件下方的限位架接触,在限位架的阻挡下立壁清灰装置速度变为0m/s,此时旋转叶完全张开,借助尾气的动力实现立壁清灰装置不间断的上下运动;所述支撑杆的一端设于阻力交变器上,所述管壁二设于支撑杆另一端,所述毛刷二设于管壁二上,毛刷二和保温组件立壁滑动接触,当立壁清灰装置沿限位杆上下运动时,毛刷二对保温组件立壁上的灰尘进行清理,利用超额行动原理实现对保温组件立壁上的灰尘进行完全清洁,并利用立壁清灰装置与限位架的碰撞将毛刷二上的灰尘抖落。Wherein, the vertical wall ash cleaning device includes a resistance alternator, a support rod, a second pipe wall and a second brush, a
其中,所述膛压滑变式自控组件包括出灰管、炉灰箱和落灰组件,所述出灰管设于底座内,所述炉灰箱设于底座上壁,所述炉灰箱包括膛压自调节滑变组件一、膛压自调节滑变组件二、拉杆口和出灰口,所述膛压自调节滑变组件一设于炉灰箱内部左侧,所述膛压自调节滑变组件二设于炉灰箱内部右侧,所述拉杆口贯穿炉灰箱侧壁设置,所述出灰口贯穿炉灰箱底壁设置,所述出灰口与出灰管相连,所述落灰组件设于炉灰箱上壁上,所述炉灰箱上壁设有通孔,所述落灰组件设于通孔上端,所述落灰组件包括复位磁性件、异形板、复位弹簧和转动轴一,所述转动轴一设于炉灰箱上壁上,所述异形板活动设于转动轴一上,所述异形板为铁磁性材料制成,复位磁性件具有磁性,所述复位磁性件设于炉灰箱上壁上,所述异形板的一端与复位磁性件活动连接,当异形板与复位磁性件接触时被复位磁性件吸引相连,所述复位弹簧的一端与炉灰箱上壁相连,异形板对通孔进行封堵,所述异形板的另一端和复位弹簧的另一端铰接,在外力的作用下异形板可绕转动轴一转动,尾气中的灰尘被清理后将堆集在异形板上,当灰尘达到一定量时,在灰尘重力的作用下,异形板克服复位弹簧的弹力和复位磁性件的吸引力绕转动轴一做逆时针转动,此时保温组件与炉灰箱连通,灰尘落到炉灰箱中。Wherein, the chamber pressure-sliding automatic control assembly includes an ash discharge pipe, a furnace ash box and an ash falling assembly, the ash discharge pipe is arranged in the base, the furnace ash box is arranged on the upper wall of the base, and the furnace ash box is arranged on the upper wall of the base. It includes chamber pressure self-adjusting sliding
优选地,所述膛压自调节滑变组件一包括限位块一、摩擦块一、摩擦块二、膛压弹簧一、膛压弹簧二、膛压控制滑块和限位块二,所述摩擦块一和膛压弹簧一设于炉灰箱侧壁上,所述限位块一设于炉灰箱侧壁上,所述限位块一位于摩擦块一和膛压弹簧一之间并紧贴摩擦块一设置,所述限位块一的长度大于摩擦块一的长度,所述膛压控制滑块活动设于炉灰箱内,在外力的作用下膛压控制滑块可在炉灰箱内左右滑动,当膛压控制滑块处于最左端时,膛压控制滑块在出灰口左侧,当膛压控制滑块处于最右端时,膛压控制滑块位于出灰口上方,膛压控制滑块对出灰口进行密封,所述摩擦块二铰接于膛压控制滑块上,所述摩擦块二与摩擦块一滑动接触,所述摩擦块一和摩擦块二的接触面为倾斜面,所述膛压弹簧二的一端设于炉灰箱上,所述膛压弹簧二的另一端设于摩擦块二上,所述限位块二设于炉灰箱内,当膛压控制滑块移动到最左端时,膛压控制滑块与限位块一接触,当膛压控制滑块移动到最右端时,膛压控制滑块与限位块二接触;所述膛压自调节滑变组件二包括限位块三、限位块四、尾气箱气压控制滑块、尾气箱弹簧和尾气箱,所述尾气箱设于炉灰箱右侧,所述尾气箱与保温组件连通,经过除尘与热能回收后的气体流入尾气箱中,所述限位块三设于炉灰箱中,所述尾气箱气压控制滑块滑动设于炉灰箱中,在外力作用下尾气箱气压控制滑块可在炉灰箱中左右滑动,所述限位块四设于尾气箱中,所述尾气箱弹簧的一端设于限位块四上,所述尾气箱弹簧的另一端设于尾气箱气压控制滑块上,所述尾气箱设有出气口一和出气口二,所述出气口一和出气口二贯穿炉灰箱底部设置,所述出气口一设于限位块四左侧,所述出气口二设于限位块四右侧,当尾气箱气压控制滑块滑动到最左端时,尾气箱气压控制滑块与出气口一脱离接触,尾气箱弹簧处于原长状态,当尾气箱气压控制滑块滑动到最右端时,尾气箱气压控制滑块覆盖在出气口一上,尾气箱气压控制滑块对出气口一进行密封;灰尘落到炉灰箱中后,由于保温管内的尾气将通过通孔进入炉灰箱中,尾气对异形板施加一个向下的力,异形板不能回复到原来的位置,落灰组件一直处于打开的状态,尾气通过通孔进入炉灰箱中,炉灰箱中的气压逐渐增大,膛压控制滑块受到向左的压力,尾气箱气压控制滑块受到向右的压力,由于摩擦块一与摩擦块二不能压缩只能相互滑动,在摩擦块二受到的向左的力大于摩擦块二与摩擦块一之间的最大静摩擦力之前,膛压控制滑块的位置始终不变,出灰口始终处于密封状态,由于尾气箱弹簧可压缩,尾气箱气压控制滑块向右移动挤压尾气箱弹簧,并对出气口一进行密封,当尾气箱气压控制滑块不能移动时,炉灰箱内的气压逐渐升高直至和保温组件内气压相等,在复位弹簧的作用下异形板回复到原来的位置,尾气通过保温组件流入到尾气箱中,由于尾气箱中的出气口一被密封,只有出气口二出气,尾气箱的进气速度高于出气速度,尾气箱的气压增大,并最终推动尾气箱气压控制滑块向左移动,使炉灰箱中的气压进一步增大,膛压控制滑块受到的向左的压力进一步增大并超过摩擦块一与摩擦块二之间的最大静摩擦力,使摩擦块二克服与摩擦块一之间的摩擦力向左滑动,摩擦块一与摩擦块二之间的摩擦力由最大静摩擦力减小为滑动摩擦力,膛压控制滑块在炉灰箱中气压的作用下快速向左移动,膛压弹簧一与膛压弹簧二被压缩,出灰口被打开,在气压的作用下炉灰箱中的灰尘经过出灰口和出灰管被吹出,炉灰箱中的气压减小,由于膛压弹簧二挤压摩擦块二,使摩擦块二与摩擦块一之间仍然有摩擦力,摩擦块二与摩擦块一之间的摩擦力和炉灰箱中气体对膛压控制滑块的合力大于膛压弹簧一的弹力,膛压控制滑块保持静止,当炉灰箱中气压与大气压相同时,灰尘不再被吹出,膛压弹簧一的弹力大于摩擦块二与摩擦块一之间的摩擦力,在膛压弹簧一的作用下膛压控制滑块克服摩擦力向右移动并与限位块二接触,再次密封出灰口;当膛压控制滑块向左移动并解除对出灰口的密封时,由于炉灰箱内气压减小,在尾气箱弹簧弹力的作用下,尾气箱气压控制滑块向右移动解除对出气口一的密封。Preferably, the first chamber pressure self-adjusting sliding variable component includes a first limit block, a first friction block, a second friction block, a first chamber pressure spring, a second chamber pressure spring, a chamber pressure control slider and a second limit block. The first friction block and the chamber pressure spring one are arranged on the side wall of the ash box, the first limit block is arranged on the side wall of the ash box, and the first limit block is located between the
其中,所述保温组件包括进气口、保温管、连接管和保温箱,所述保温箱设于炉灰箱上,所述保温管设于保温箱内,保温箱对保温管进行支撑固定,所述保温管底部设有贯穿孔二和保温管缩口,所述贯穿孔二设于异形板上部,保温组件中被清理后的烟尘通过保温管底部的贯穿孔落于异形板上,所述保温管缩口设于自旋转固气单向分离装置下部,保温管缩口的内径与毛刷圆筒的内径相同,使被清理到毛刷一的一端的灰尘能够绕过缩口落到异形板上,不会被尾气再次吹起;所述连接管的一端设于保温管上,所述连接管的另一端设于尾气箱上,将被清除烟尘和回收热能后的尾气通入尾气箱中,所述进气口设于保温管上部,使灰尘不会堆积堵塞进气口。Wherein, the heat preservation assembly includes an air inlet, a heat preservation pipe, a connecting pipe and a heat preservation box, the heat preservation box is arranged on the ash box, the heat preservation pipe is arranged in the heat preservation box, and the heat preservation box supports and fixes the heat preservation pipe, The bottom of the heat preservation pipe is provided with a second through hole and a constriction of the heat preservation pipe. The second through hole is set on the upper part of the special-shaped plate, and the cleaned smoke and dust in the heat preservation assembly falls on the special-shaped plate through the through hole at the bottom of the heat preservation pipe. The shrinkage of the insulation pipe is set at the lower part of the self-rotating solid-gas one-way separation device. The inner diameter of the shrinkage of the insulation pipe is the same as the inner diameter of the brush cylinder, so that the dust cleaned to one end of the brush can bypass the shrinkage and fall to the special shape. On the board, it will not be blown up again by the exhaust gas; one end of the connecting pipe is set on the insulation pipe, and the other end of the connecting pipe is set on the tail gas box, and the exhaust gas after removing smoke and dust and recovering heat energy is passed into the tail gas box. , the air inlet is arranged on the upper part of the insulation pipe, so that dust will not accumulate and block the air inlet.
优选地,所述保温箱与保温管填充有保温材料,防止尾气中的热量在过滤器中流失。Preferably, the insulation box and the insulation pipe are filled with insulation materials to prevent the heat in the exhaust gas from being lost in the filter.
优选地,所述底座设有出气通道一、出气通道二和出气通道三,所述出气通道一设于底座内,所述出气通道一与出气口一连通,所述出气通道二设于底座内,所述出气通道二与出气口二连通,所述出气通道三设于底座内,所述出气通道三与出气通道一和出气通道二相连,净化后的尾气从尾气箱流出后,经过出气通道一和出气通道二流向出气通道三,并从出气通道三中流向余热锅炉进行。Preferably, the base is provided with an
其中,所述膛压控制滑块设有螺纹孔,当维修时通过拉杆口和螺纹孔可将膛压控制滑块向左拉动,出灰口被打开,将抽风机与出灰口连接并抽风,可将保温管与炉灰箱中的残留灰尘进行清理。The chamber pressure control slider is provided with a threaded hole. During maintenance, the chamber pressure control slider can be pulled to the left through the tie rod port and the threaded hole, the ash outlet is opened, and the exhaust fan is connected to the ash outlet to extract air. , the residual dust in the insulation pipe and the ash box can be cleaned up.
其中,所述毛刷一与毛刷二的材质为硅酸铝纤维,可以承受1700℃的高温,使本装置能够适用金属冶炼等行业余热回收的预除尘操作。The first and second brushes are made of aluminum silicate fibers, which can withstand a high temperature of 1700°C, so that the device can be applied to pre-dust removal operations for waste heat recovery in industries such as metal smelting.
采用上述结构本发明取得的有益效果如下:The beneficial effects obtained by adopting the above-mentioned structure of the present invention are as follows:
(1)利用立壁清灰装置,使保温管不会在使用时因为灰尘沉积发生堵塞,借助阻力交变器与毛刷二的设计实现立壁清灰装置的无动力往复自由移动,利用超额行动原理实现对保温组件立壁上的灰尘进行完全清洁。(1) The vertical wall cleaning device is used to prevent the thermal insulation pipe from being blocked due to dust deposition during use. With the help of the design of the resistance alternator and the second brush, the vertical wall cleaning device can be freely moved back and forth without power, and the principle of excess action is used. Completely clean the dust on the vertical wall of the thermal insulation component.
(2)利用自旋转固气单向分离装置和固气的密度与体积差异,使气体能够通过毛刷一继续流动,固体烟尘再与毛刷一接触口失去动能并在重力的作用下下落,毛刷一的设置隔绝了气流对固体烟尘的影响,实现固体烟尘与气体的分离。(2) Using the self-rotating solid-gas one-way separation device and the difference in density and volume of solid-gas, the gas can continue to flow through the brush, and the solid smoke loses kinetic energy when it contacts the brush and falls under the action of gravity. The setting of the
(3)保温管缩口的设置为烟尘提供了一个稳定的存放区,使烟尘在堆积后不会再收到向上的作用力随气流继续运动,通过可活动落灰组件的设计,利用气流易流向易通过路径的特点,使推积在异形板上的烟尘可以被完全吹入炉灰箱中。(3) The setting of the constriction of the insulation pipe provides a stable storage area for the smoke and dust, so that the smoke and dust will not receive upward force and continue to move with the airflow after accumulation. The characteristics of the flow direction are easy to pass, so that the dust accumulated on the special-shaped plate can be completely blown into the ash box.
(4)保温管内瓷质涂层的设计,一方面减少热量的损失,另一方面减小尾气对管道的腐蚀。(4) The design of the porcelain coating in the insulation pipe reduces heat loss on the one hand, and reduces the corrosion of the pipe by exhaust gas on the other hand.
(5)利用最大静摩擦力大于滑动摩擦力的特点,使膛压控制滑块可以在达到临界压力后快速移动,使炉灰箱中能够累积足够的气压,达到对炉灰箱中的烟尘进行充分清理的目的。(5) Utilizing the feature that the maximum static friction force is greater than the sliding friction force, the chamber pressure control slider can move quickly after reaching the critical pressure, so that sufficient air pressure can be accumulated in the ash box to achieve sufficient dust removal in the ash box. purpose of cleaning.
(6)膛压自调节滑变组件一与膛压自调节滑变组件二的设计,实现了无动力烟尘自动高压循环清洁,通过简单的机械结构设计减少了人工操作投入。(6) The design of chamber pressure self-adjusting sliding
附图说明Description of drawings
图1为本发明提供的一种尾气粉尘分离过滤器的剖视图;Fig. 1 is a sectional view of a kind of tail gas dust separation filter provided by the present invention;
图2为本发明提供的一种尾气粉尘分离过滤器的限位架的结构示意图;2 is a schematic structural diagram of a limit frame of a tail gas dust separation filter provided by the present invention;
图3为图1的A处的局部放大图;Fig. 3 is a partial enlarged view at A of Fig. 1;
图4为本发明提供的一种尾气粉尘分离过滤器的落灰组件的剖视图4 is a cross-sectional view of the ash falling component of a tail gas dust separation filter provided by the present invention
图5为本发明提供的一种尾气粉尘分离过滤器的限位杆的结构示意图;5 is a schematic structural diagram of a limit rod of a tail gas dust separation filter provided by the present invention;
图6为本发明提供的一种尾气粉尘分离过滤器的限位杆的俯视图;6 is a top view of a limit rod of a tail gas dust separation filter provided by the present invention;
图7为图1的B处的局部放大图;Fig. 7 is a partial enlarged view at B of Fig. 1;
图8为图1的C处的局部放大图;Fig. 8 is a partial enlarged view at C of Fig. 1;
图9为本发明提供的一种尾气粉尘分离过滤器的自旋转固气单向分离装置的结构示意图;9 is a schematic structural diagram of a self-rotating solid-gas one-way separation device of a tail gas dust separation filter provided by the present invention;
图10为本发明提供的一种尾气粉尘分离过滤器的中轴的结构示意图;10 is a schematic structural diagram of a central axis of a tail gas dust separation filter provided by the present invention;
图11为本发明提供的一种尾气粉尘分离过滤器的转动扇的结构示意图;11 is a schematic structural diagram of a rotating fan of a tail gas dust separation filter provided by the present invention;
图12为本发明提供的一种尾气粉尘分离过滤器的除尘板的结构示意图;12 is a schematic structural diagram of a dust removal plate of a tail gas dust separation filter provided by the present invention;
图13为本发明提供的一种尾气粉尘分离过滤器的毛刷一的结构示意图;13 is a schematic structural diagram of a
图14为本发明提供的一种尾气粉尘分离过滤器的立壁清灰装置的结构示意图;14 is a schematic structural diagram of a vertical wall ash cleaning device of a tail gas dust separation filter provided by the present invention;
图15为本发明提供的一种尾气粉尘分离过滤器的阻力交变器的结构示意图;15 is a schematic structural diagram of a resistance alternator of a tail gas dust separation filter provided by the present invention;
图16为本发明提供的一种尾气粉尘分离过滤器的旋转叶的结构示意图;16 is a schematic structural diagram of a rotating blade of a tail gas dust separation filter provided by the present invention;
图17为图15的D处的局部放大图;Fig. 17 is a partial enlarged view at D of Fig. 15;
图18为本发明提供的一种尾气粉尘分离过滤器的第五齿轮的结构示意图;18 is a schematic structural diagram of the fifth gear of a tail gas dust separation filter provided by the present invention;
图19为本发明提供的一种尾气粉尘分离过滤器的转动盘的俯视图一;Figure 19 is a
图20为本发明提供的一种尾气粉尘分离过滤器的转动盘的俯视图二;Fig. 20 is the top view two of the rotating disk of a kind of tail gas dust separation filter provided by the present invention;
图21为本发明提供的一种尾气粉尘分离过滤器的固定盘的俯视图。FIG. 21 is a top view of a fixed plate of a tail gas dust separation filter provided by the present invention.
其中,1、保温组件,2、自旋转固气单向分离装置,3、立壁清灰装置,4、膛压滑变式自控组件,5、底座,6、限位架,7、限位杆,8、螺纹孔,11、进气口,12、保温管,13、连接管,14、保温箱,15、贯穿孔二,16、保温管缩口,21、管壁一,22、转动扇,23、中轴,24、毛刷一,25、密封轴承,26、上支架,27、下支架,28、除尘板,31、阻力交变器,32、支撑杆,33、管壁二,34、毛刷二,35、贯穿孔一,311、顶盘,312、旋转叶,313、转动盘,314、固定盘,315、传动机构,316、限位凸点,3131、滑动槽二,3132、内齿,3141、固定螺栓,3142、固定柱,3143、外齿,3144、缺口,3151、转动轴二,3152、转动轴三,3153、动力轮,3154、第一齿轮,3155、第二齿轮,3156、牙盘,3157、第三齿轮,3158、第四齿轮,3159、第五齿轮,31510、第六齿轮,31511、第七齿轮,41、出灰管,42、炉灰箱,43、落灰组件,421、膛压自调节滑变组件一,422、膛压自调节滑变组件二,423、拉杆口,424、出灰口,425、通孔,431、复位磁性件,432、异形板,433、复位弹簧,434、转动轴一,4211、限位块一,4212、摩擦块一,4213、摩擦块二,4214、膛压弹簧一,4215、膛压弹簧二,4216、膛压控制滑块,4217、限位块二,4221、限位块三,4222、限位块四,4223、尾气箱气压控制滑块,4224、尾气箱弹簧,4225、尾气箱,4226、出气口一,4227、出气口二,51、出气通道一,52、出气通道二,53、出气通道三,71、滑动槽一。Among them, 1. Thermal insulation component, 2. Self-rotating solid-gas one-way separation device, 3. Vertical wall ash cleaning device, 4. Chamber pressure sliding automatic control component, 5. Base, 6. Limiting frame, 7. Limiting rod , 8, threaded hole, 11, air inlet, 12, insulation pipe, 13, connecting pipe, 14, insulation box, 15, through hole two, 16, insulation pipe shrinkage, 21, pipe wall one, 22, rotating fan , 23, central axis, 24, brush one, 25, sealed bearing, 26, upper bracket, 27, lower bracket, 28, dust removal board, 31, resistance alternator, 32, support rod, 33, pipe wall two, 34, brush two, 35, through hole one, 311, top plate, 312, rotating blade, 313, rotating plate, 314, fixed plate, 315, transmission mechanism, 316, limit bump, 3131, sliding groove two, 3132, inner teeth, 3141, fixing bolts, 3142, fixing column, 3143, outer teeth, 3144, notches, 3151, rotating shaft two, 3152, rotating shaft three, 3153, power wheel, 3154, first gear, 3155, first 2nd gear, 3156, crankset, 3157, 3rd gear, 3158, 4th gear, 3159, 5th gear, 31510, 6th gear, 31511, 7th gear, 41, ash outlet, 42, ash box, 43. Ash falling component, 421, Chamber pressure self-adjusting sliding
附图用来提供对本发明的进一步理解,并且构成说明书的一部分,与本发明的实施例一起用于解释本发明,并不构成对本发明的限制。The accompanying drawings are used to provide a further understanding of the present invention, and constitute a part of the specification, and are used to explain the present invention together with the embodiments of the present invention, and do not constitute a limitation to the present invention.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例;基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments; based on the The embodiments of the present invention, and all other embodiments obtained by those of ordinary skill in the art without creative work, fall within the protection scope of the present invention.
在本发明的描述中,需要理解的是,术语“上”、“下”、“前”、“后”、“左”、“右”、“顶”、“底”、“内”、“外”等指示方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。In the description of the present invention, it should be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inside", " “Outside” and other indications of orientation or positional relationship are based on the orientation or positional relationship shown in the accompanying drawings, which are only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the referred device or element must have a specific orientation, a specific orientation, and a specific orientation. The orientation configuration and operation of the device should not be construed as a limitation of the present invention.
如图1、图2、图3、图5、图6、图9、图10、图11、图12和图13所示,本发明一种尾气粉尘分离过滤器,包括保温组件1、自旋转固气单向分离装置2、立壁清灰装置3和膛压滑变式自控组件4和底座5;膛压滑变式自控组件4设于底座5上,底座5对膛压滑变式自控组件4进行支撑固定,保温组件1设于膛压滑变式自控组件4上,自旋转固气单向分离装置2设于保温组件1内,保温组件1对自旋转固气单向分离装置2进行支撑固定,立壁清灰装置3活动设于保温组件1内,立壁清灰装置3位于自旋转固气单向分离装置2上方,自旋转固气单向分离装置2和立壁清灰装置3设有若干组,在尾气的带动下立壁清灰装置3不断上下运动,对保温组件1立壁上的灰尘进行清理;保温组件1内设有限位架6,限位架6设有若干组,限位架6之间设有限位杆7,限位杆7呈竖直方向设置,自旋转固气单向分离装置2包括管壁一21、转动扇22、中轴23、毛刷一24和密封轴承25,管壁一21设于保温组件1内,保温组件1对管壁一21进行支撑固定,毛刷一24的一端设于管壁一21内壁,毛刷一24的另一端设有绒毛,毛刷一24的一端为光杆设置,毛刷一24设有若干组,若干组毛刷一24组合为毛刷圆筒,密封轴承25的外圈设于限位架6上,中轴23设于密封轴承25的内圈上,限位架6对密封轴承25和中轴23进行支撑固定,在外力的带动下中轴23和密封轴承25内圈做同轴转动,转动扇22设于中轴23上,转动扇22设有若干组,转动扇22倾斜设置,中轴23上设有上支架26和下支架27,上支架26的一端和下支架27的一端设于中轴23上,上支架26的另一端和下支架27的另一端设有除尘板28,除尘板28设有若干组,除尘板28活动设于毛刷一24中,除尘板28倾斜设置,当锅炉的尾气通过保温组件1流经自旋转固气单向分离装置2时,尾气将驱动转动扇22转动,转动扇22带动中轴23、上支架26、下支架27和除尘板28做同心转动,由于转动扇22倾斜的设于中轴23上,原本竖直方向流动的气体遇到转动扇22时将对转动扇22产生一个水平方向的分力,推动转动扇22旋转,由于力的作用是相互的,转动扇22将给气体施加一个水平方向的反作用力,转动扇22通过对气体施加的水平方向的反作用力推动粉尘飞入毛刷一24中,除尘板28和转动扇22做同心转动且除尘板28伸入毛刷一24中,除尘板28拍打毛刷一24,使毛刷一24上的粉尘在除尘板28和惯性力的作用下运动到毛刷一24的一端,毛刷一24的另一端的绒毛部分阻挡了高速气流的通过,毛刷一24的一端与管壁一21组成了一个对于固体粉尘无阻力的下沉通道,且在毛刷一24的另一端的绒毛中气体的密度小、体积小,尾气中的气体能够通过绒毛自由流动并上升,而粉尘作为固体颗粒密度大、体积大,在通过绒毛时阻力更大难以运动,在绒毛中流动的气体不再有足够的流速带动粉尘继续运动,粉尘被除尘板28拍进毛刷一24的一端内,在重力的作用下不断下降堆积,实现了对于气体低阻力、对于固体高阻力的设计,并在气体流动过程中除尘的功能。As shown in Fig. 1, Fig. 2, Fig. 3, Fig. 5, Fig. 6, Fig. 9, Fig. 10, Fig. 11, Fig. 12 and Fig. 13, an exhaust gas dust separation filter of the present invention comprises a
如图1、图2、图5、图6、图14、图15、图16、图17、图18、图19、图20和图21所示,立壁清灰装置3包括阻力交变器31、支撑杆32、管壁二33和毛刷二34,阻力交变器31中间设有贯穿孔一35,限位杆7通过贯穿孔一35贯穿阻力交变器31设置,在外力的作用下阻力交变器31可沿限位杆7上下滑动,阻力交变器31包括顶盘311、旋转叶312、转动盘313、固定盘314和传动机构315,固定盘314和限位杆7滑动连接,固定盘314上设有限位凸点316,限位杆7上设有滑动槽一71,滑动槽一71内表面光滑设置,限位凸点316卡入滑动槽一71中,当固定盘314沿限位杆7上下滑动时,一方面限位杆7使固定盘314只能沿竖直方向运动,另一方面限位杆7使固定盘314在沿竖直方向运动时不会发生转动;固定盘314上设有固定螺栓3141、固定柱3142和外齿3143,转动盘313活动设于固定盘314上,转动盘313上设有滑动槽二3131,滑动槽二3131贯穿转动盘313设置,转动盘313上设有内齿3132,固定螺栓3141和固定柱3142设于滑动槽二3131内,当转动盘313受到外力作用时,滑动槽二3131可沿固定螺栓3141滑动,固定螺栓3141和固定柱3142对滑动槽二3131的移动起到限位作用,外齿3143与内齿3132相对设置,内齿3132与外齿3143组成一个带有内部轮齿的凹槽,固定螺栓3141上表面与转动盘313上表面齐平,固定柱3142上表面高于转动盘313上表面,顶盘311设于固定柱3142上,固定柱3142对顶盘311进行支撑固定;传动机构315包括转动轴二3151、转动轴三3152、动力轮3153、第一齿轮3154、第二齿轮3155、牙盘3156、第三齿轮3157、第四齿轮3158、第五齿轮3159、第六齿轮31510和第七齿轮31511,固定盘314设有缺口3144,转动轴二3151、转动轴三3152设于缺口3144侧壁上,缺口3144对转动轴二3151和转动轴三3152进行支撑和固定,动力轮3153活动设于转动轴二3151上,当阻力交变器31沿限位杆7上下移动时,动力轮3153在限位杆7表面滚动,动力轮3153与限位杆7之间竖直方向的作用力为静摩擦力,在外力的作用下动力轮3153可绕转动轴二3151转动,牙盘3156活动设于转动轴三3152上,在外力的作用下牙盘3156可绕转动轴三3152转动,第一齿轮3154设于动力轮3153上,第二齿轮3155设于牙盘3156上,第一齿轮3154与第二齿轮3155相互啮合,第三齿轮3157、第四齿轮3158、第五齿轮3159和第七齿轮31511活动设于固定盘314上,第三齿轮3157与牙盘3156相互啮合,第四齿轮3158与第三齿轮3157相互啮合,第五齿轮3159为不完全齿轮,第五齿轮3159与外齿3143相啮合,第五齿轮3159在活动范围内只能和外齿3143相互啮合,不能与内齿3132啮合,第七齿轮31511与内齿3132和外齿3143相互啮合,第六齿轮31510设于第五齿轮3159上,第六齿轮31510与第四齿轮3158啮合,旋转叶312设于第七齿轮31511上,旋转叶312随第七齿轮31511的转动而转动,初始时,立壁清灰装置3位于保温组件1底部,旋转叶312处于张开状态,当通入尾气后,由于旋转叶312对气流的阻力大,气流对立壁清灰装置3向上的力大于立壁清灰装置3受到的向下的力,立壁清灰装置3在气流的作用下将沿限位杆7向上做加速运动,在立壁清灰装置3的带动下动力轮3153沿限位杆7顺时针向上滚动,并带动第一齿轮3154顺时针转动,第一齿轮3154带动第二齿轮3155和牙盘3156做逆时针转动,牙盘3156带动第三齿轮3157做顺时针转动,第三齿轮3157带动第四齿轮3158逆时针转动,第四齿轮3158带动第六齿轮31510和第五齿轮3159顺时针转动,第五齿轮3159带动外齿3143顺时针转动,外齿3143带动转动盘313绕限位杆7做顺时针转动,同时外齿3143带动第七齿轮31511在顺时针自传的同时沿内齿3132做顺时针公转,在第七齿轮31511的带动下旋转叶312逐渐闭合,阻力交变器31受到向上的力逐渐变小,并最终小于向下的力,立壁清灰装置3向上运动的速度变化由向上加速变为向上减速,在立壁清灰装置3向上运动的速度降为0m/s之前,立壁清灰装置3与保温组件1上方的限位架6接触,在限位架6的阻挡下立壁清灰装置3速度变为0m/s,此时旋转叶312已经完全收回到阻力交变器31中,随后立壁清灰装置3在重力的作用下向下加速运动,在立壁清灰装置3的带动下动力轮3153沿限位杆7逆时针滚动,并带动第一齿轮3154逆时针转动,第一齿轮3154带动第二齿轮3155和牙盘3156做顺时针转动,牙盘3156带动第三齿轮3157做逆时针转动,第三齿轮3157带动第四齿轮3158顺时针转动,第四齿轮3158带动第六齿轮31510和第五齿轮3159逆时针转动,第五齿轮3159带动外齿3143逆时针转动,外齿3143带动转动盘313绕限位杆7做逆时针转动,同时外齿3143带动第七齿轮31511在顺时针自传的同时沿内齿3132做逆时针公转,在第七齿轮31511的带动下旋转叶312逐渐张开,阻力交变器31受到向上的力逐渐变大,并最终大于向下的力,立壁清灰装置3向下运动的速度变化由向下加速变为向下减速,在立壁清灰装置3向下运动的速度降为0m/s之前,立壁清灰装置3与保温组件1下方的限位架6接触,在限位架6的阻挡下立壁清灰装置3速度变为0m/s,此时旋转叶312完全张开,借助尾气的动力实现立壁清灰装置3不间断的上下运动;支撑杆32的一端设于阻力交变器31上,管壁二33设于支撑杆32另一端,毛刷二34设于管壁二33上,毛刷二34和保温组件1立壁滑动接触,当立壁清灰装置3沿限位杆7上下运动时,毛刷二34对保温组件1立壁上的灰尘进行清理,利用超额行动原理实现对保温组件1立壁上的灰尘进行完全清洁,并利用立壁清灰装置3与限位架6的碰撞将毛刷二34上的灰尘抖落。As shown in Figure 1, Figure 2, Figure 5, Figure 6, Figure 14, Figure 15, Figure 16, Figure 17, Figure 18, Figure 19, Figure 20 and Figure 21, the vertical wall
如图1、图3、图4、图7和图8所示,膛压滑变式自控组件4包括出灰管41、炉灰箱42和落灰组件43,出灰管41设于底座5内,炉灰箱42设于底座5上壁,炉灰箱42包括膛压自调节滑变组件一421、膛压自调节滑变组件二422、拉杆口423和出灰口424,膛压自调节滑变组件一421设于炉灰箱42内部左侧,膛压自调节滑变组件二422设于炉灰箱42内部右侧,拉杆口423贯穿炉灰箱42侧壁设置,出灰口424贯穿炉灰箱42底壁设置,出灰口424与出灰管41相连,落灰组件43设于炉灰箱42上壁上,炉灰箱42上壁设有通孔425,落灰组件43设于通孔425上端,落灰组件43包括复位磁性件431、异形板432、复位弹簧433和转动轴一434,转动轴一434设于炉灰箱42上壁上,异形板432活动设于转动轴一434上,异形板432为铁磁性材料制成,复位磁性件431具有磁性,复位磁性件431设于炉灰箱42上壁上,异形板432的一端与复位磁性件431活动连接,当异形板432与复位磁性件431接触时被复位磁性件431吸引相连,复位弹簧433的一端与炉灰箱42上壁相连,异形板432对通孔425进行封堵,异形板432的另一端和复位弹簧433的另一端铰接,在外力的作用下异形板432可绕转动轴一434转动,尾气中的灰尘被清理后将堆集在异形板432上,当灰尘达到一定量时,在灰尘重力的作用下,异形板432克服复位弹簧433的弹力和复位磁性件431的吸引力绕转动轴一434做逆时针转动,此时保温组件1与炉灰箱42连通,灰尘落到炉灰箱42中。As shown in Figure 1, Figure 3, Figure 4, Figure 7 and Figure 8, the chamber pressure sliding type automatic control assembly 4 includes an ash discharge pipe 41, a
如图1、图3、图4、图7和图8所示,膛压自调节滑变组件一421包括限位块一4211、摩擦块一4212、摩擦块二4213、膛压弹簧一4214、膛压弹簧二4215、膛压控制滑块4216和限位块二4217,摩擦块一4212和膛压弹簧一4214设于炉灰箱42侧壁上,限位块一4211设于炉灰箱42侧壁上,限位块一4211位于摩擦块一4212和膛压弹簧一4214之间并紧贴摩擦块一4212设置,限位块一4211的长度大于摩擦块一4212的长度,膛压控制滑块4216活动设于炉灰箱42内,在外力的作用下膛压控制滑块4216可在炉灰箱42内左右滑动,当膛压控制滑块4216处于最左端时,膛压控制滑块4216在出灰口424左侧,当膛压控制滑块4216处于最右端时,膛压控制滑块4216位于出灰口424上方,膛压控制滑块4216对出灰口424进行密封,摩擦块二4213铰接于膛压控制滑块4216上,摩擦块二4213与摩擦块一4212滑动接触,摩擦块一4212和摩擦块二4213的接触面为倾斜面,膛压弹簧二4215的一端设于炉灰箱42上,膛压弹簧二4215的另一端设于摩擦块二4213上,限位块二4217设于炉灰箱42内,当膛压控制滑块4216移动到最左端时,膛压控制滑块4216与限位块一4211接触,当膛压控制滑块4216移动到最右端时,膛压控制滑块4216与限位块二4217接触;膛压自调节滑变组件二422包括限位块三4221、限位块四4222、尾气箱气压控制滑块4223、尾气箱弹簧4224和尾气箱4225,尾气箱4225设于炉灰箱42右侧,尾气箱4225与保温组件1连通,经过除尘与热能回收后的气体流入尾气箱4225中,限位块三4221设于炉灰箱42中,尾气箱气压控制滑块4223滑动设于炉灰箱42中,在外力作用下尾气箱气压控制滑块4223可在炉灰箱42中左右滑动,限位块四4222设于尾气箱4225中,尾气箱弹簧4224的一端设于限位块四4222上,尾气箱弹簧4224的另一端设于尾气箱气压控制滑块4223上,尾气箱4225设有出气口一4226和出气口二4227,出气口一4226和出气口二4227贯穿炉灰箱42底部设置,出气口一4226设于限位块四4222左侧,出气口二4227设于限位块四4222右侧,当尾气箱气压控制滑块4223滑动到最左端时,尾气箱气压控制滑块4223与出气口一4226脱离接触,尾气箱弹簧4224处于原长状态,当尾气箱气压控制滑块4223滑动到最右端时,尾气箱气压控制滑块4223覆盖在出气口一4226上,尾气箱气压控制滑块4223对出气口一4226进行密封;灰尘落到炉灰箱42中后,由于保温管12内的尾气将通过通孔425进入炉灰箱42中,尾气对异形板432施加一个向下的力,异形板432不能回复到原来的位置,落灰组件43一直处于打开的状态,尾气通过通孔425进入炉灰箱42中,炉灰箱42中的气压逐渐增大,膛压控制滑块4216受到向左的压力,尾气箱气压控制滑块4223受到向右的压力,由于摩擦块一4212与摩擦块二4213不能压缩只能相互滑动,在摩擦块二4213受到的向左的力大于摩擦块二4213与摩擦块一4212之间的最大静摩擦力之前,膛压控制滑块4216的位置始终不变,出灰口424始终处于密封状态,由于尾气箱弹簧4224可压缩,尾气箱气压控制滑块4223向右移动挤压尾气箱弹簧4224,并对出气口一4226进行密封,当尾气箱气压控制滑块4223不能移动时,炉灰箱42内的气压逐渐升高直至和保温组件1内气压相等,在复位弹簧433的作用下异形板432回复到原来的位置,尾气通过保温组件1流入到尾气箱4225中,由于尾气箱4225中的出气口一4226被密封,只有出气口二4227出气,尾气箱4225的进气速度高于出气速度,尾气箱4225的气压增大,并最终推动尾气箱气压控制滑块4223向左移动,使炉灰箱42中的气压进一步增大,膛压控制滑块4216受到的向左的压力进一步增大并超过摩擦块一4212与摩擦块二4213之间的最大静摩擦力,使摩擦块二4213克服与摩擦块一4212之间的摩擦力向左滑动,摩擦块一4212与摩擦块二4213之间的摩擦力由最大静摩擦力减小为滑动摩擦力,膛压控制滑块4216在炉灰箱42中气压的作用下快速向左移动,膛压弹簧一4214与膛压弹簧二4215被压缩,出灰口424被打开,在气压的作用下炉灰箱42中的灰尘经过出灰口424和出灰管41被吹出,炉灰箱42中的气压减小,由于膛压弹簧二4215挤压摩擦块二4213,使摩擦块二4213与摩擦块一4212之间仍然有摩擦力,摩擦块二4213与摩擦块一4212之间的摩擦力和炉灰箱42中气体对膛压控制滑块4216的合力大于膛压弹簧一4214的弹力,膛压控制滑块4216保持静止,当炉灰箱42中气压与大气压相同时,灰尘不再被吹出,膛压弹簧一4214的弹力大于摩擦块二4213与摩擦块一4212之间的摩擦力,在膛压弹簧一4214的作用下膛压控制滑块4216克服摩擦力向右移动并与限位块二4217接触,再次密封出灰口424;当膛压控制滑块4216向左移动并解除对出灰口424的密封时,由于炉灰箱42内气压减小,在尾气箱弹簧4224弹力的作用下,尾气箱气压控制滑块4223向右移动解除对出气口一4226的密封。As shown in Figure 1, Figure 3, Figure 4, Figure 7 and Figure 8, the chamber pressure self-adjusting sliding
如图1、图3、图4、图7和图8所示,保温组件1包括进气口11、保温管12、连接管13和保温箱14,保温箱14设于炉灰箱42上,保温管12设于保温箱14内,保温箱14对保温管12进行支撑固定,保温管12底部设有贯穿孔二15和保温管缩口16,贯穿孔二15设于异形板432上部,保温组件1中被清理后的烟尘通过保温管12底部的贯穿孔落于异形板432上,保温管缩口16设于自旋转固气单向分离装置2下部,保温管缩口16的内径与毛刷圆筒的内径相同,使被清理到毛刷一24的一端的灰尘能够绕过缩口落到异形板432上,不会被尾气再次吹起;连接管13的一端设于保温管12上,连接管13的另一端设于尾气箱4225上,将被清除烟尘和回收热能后的尾气通入尾气箱4225中,进气口11设于保温管12上部,使灰尘不会堆积堵塞进气口11。As shown in Figure 1, Figure 3, Figure 4, Figure 7 and Figure 8, the
如图1、图6、图7、图9、图13和图14所示,保温箱14与保温管12填充有保温材料,防止尾气中的热量在过滤器中流失,底座5设有出气通道一51、出气通道二52和出气通道三53,出气通道一51设于底座5内,出气通道一51与出气口一4226连通,出气通道二52设于底座5内,出气通道二52与出气口二4227连通,出气通道三53设于底座5内,出气通道三53与出气通道一51和出气通道二52相连,净化后的尾气从尾气箱4225流出后,经过出气通道一51和出气通道二52流向出气通道三53,并从出气通道三53中流向余热锅炉进行,膛压控制滑块4216设有螺纹孔8,当维修时通过拉杆口423和螺纹孔8可将膛压控制滑块4216向左拉动,出灰口424被打开,将抽风机与出灰口424连接并抽风,可将保温管12与炉灰箱42中的残留灰尘进行清理,毛刷一24与毛刷二34的材质为硅酸铝纤维。As shown in Figure 1, Figure 6, Figure 7, Figure 9, Figure 13 and Figure 14, the
具体使用时,将出气通道三53与余热锅炉相连,高温尾气从进气口11流入后保温管12后,依次通过自旋转固气单向分离装置2、立壁清灰装置3、连接管13和尾气箱4225,当高温尾气通过保温组件1流经自旋转固气单向分离装置2时,尾气将驱动转动扇22转动,转动扇22带动中轴23、上支架26、下支架27和除尘板28做同心转动,由于转动扇22倾斜的设于中轴23上,原本竖直方向流动的气体遇到转动扇22时将对转动扇22产生一个水平方向的分力,推动转动扇22旋转,由于力的作用是相互的,转动扇22将给气体施加一个水平方向的反作用力,转动扇22通过对气体施加的水平方向的反作用力推动粉尘飞入毛刷一24中,除尘板28和转动扇22做同心转动且除尘板28伸入毛刷一24中,除尘板28拍打毛刷一24,使毛刷一24上的粉尘在除尘板28和惯性力的作用下运动到毛刷一24的一端,毛刷一24的另一端的绒毛部分阻挡了高速气流的通过,毛刷一24的一端与管壁一21组成了一个对于固体粉尘无阻力的下沉通道,且在毛刷一24的另一端的绒毛中气体的密度小、体积小,尾气中的气体能够通过绒毛自由流动并上升,而粉尘作为固体颗粒密度大、体积大,在通过绒毛时阻力更大难以运动,在绒毛中流动的气体不再有足够的流速带动粉尘继续运动,粉尘被除尘板28拍进毛刷一24的一端内,在重力的作用下不断下降堆积在落灰组件43上,初始时立壁清灰装置3静置于底部的限位架6上,旋转叶312处于张开状态,当尾气流经立壁清灰装置3后,由于旋转叶312对气流的阻力大,气流对立壁清灰装置3向上的力大于立壁清灰装置3收到的向下的力,立壁清灰装置3在气流的作用下将沿限位杆7向上做加速运动,在立壁清灰装置3的带动下动力轮3153沿限位杆7顺时针滚动,并带动第一齿轮3154顺时针转动,第一齿轮3154带动第二齿轮3155和牙盘3156做逆时针转动,牙盘3156带动第三齿轮3157做顺时针转动,第三齿轮3157带动第四齿轮3158逆时针转动,第四齿轮3158带动第六齿轮31510和第五齿轮3159顺时针转动,第五齿轮3159带动外齿3143顺时针转动,外齿3143带动转动盘313绕限位杆7做顺时针转动,同时外齿3143带动第七齿轮31511在顺时针自传的同时沿内齿3132做顺时针公转,在第七齿轮31511的带动下旋转叶312逐渐闭合,阻力交变器31受到向上的力逐渐变小,并最终小于向下的力,立壁清灰装置3向上运动的速度变化由向上加速变为向上减速,在立壁清灰装置3向上运动的速度降为0m/s之前,立壁清灰装置3与保温组件1上方的限位架6接触,在限位架6的阻挡下立壁清灰装置3速度变为0m/s,此时旋转叶312已经完全收回到阻力交变器31中,随后立壁清灰装置3在重力的作用下向下加速运动,在立壁清灰装置3的带动下动力轮3153沿限位杆7逆时针滚动,并带动第一齿轮3154逆时针转动,第一齿轮3154带动第二齿轮3155和牙盘3156做顺时针转动,牙盘3156带动第三齿轮3157做逆时针转动,第三齿轮3157带动第四齿轮3158顺时针转动,第四齿轮3158带动第六齿轮31510和第五齿轮3159逆时针转动,第五齿轮3159带动外齿3143逆时针转动,外齿3143带动转动盘313绕限位杆7做逆时针转动,同时外齿3143带动第七齿轮31511在顺时针自传的同时沿内齿3132做逆时针公转,在第七齿轮31511的带动下旋转叶312逐渐张开,阻力交变器31受到向上的力逐渐变大,并最终大于向下的力,立壁清灰装置3向下运动的速度变化由向下加速变为向下减速,在立壁清灰装置3向下运动的速度降为0m/s之前,立壁清灰装置3与保温组件1下方的限位架6接触,在限位架6的阻挡下立壁清灰装置3速度变为0m/s,此时旋转叶312完全张开,借助尾气的动力实现立壁清灰装置3不间断的上下运动;支撑杆32的一端设于阻力交变器31上,管壁二33设于支撑杆32另一端,毛刷二34设于管壁二33上,毛刷二34和保温组件1立壁滑动接触,当立壁清灰装置3沿限位杆7上下运动时,毛刷二34对保温组件1立壁上的灰尘进行清理,利用超额行动原理实现对保温组件1立壁上的灰尘进行完全清洁,并利用立壁清灰装置3与限位架6的碰撞将毛刷二34上的灰尘抖落,抖落的灰尘通过毛刷一24的一端与管壁一21组成的对于固体粉尘无阻力的下沉通道和保温管缩口16外侧落在落灰组件43上,随着落灰组件43上烟尘的增多,在灰尘重力的作用下,异形板432克服复位弹簧433的弹力和复位磁性件431的吸引力绕转动轴一434做逆时针转动,此时保温组件1与炉灰箱42连通,灰尘落到炉灰箱42中;灰尘落到炉灰箱42中后,由于保温管12内的气流将冲入炉灰箱42中,并对异形板432施加一个向下的压力,异形板432不能回复到原来的位置,落灰组件43一直处于打开的状态,尾气通过通孔425进入炉灰箱42中,炉灰箱42中的气压逐渐增大,膛压控制滑块4216受到向左的压力,尾气箱气压控制滑块4223受到向右的压力,由于摩擦块一4212与摩擦块二4213不能压缩只能相互滑动,在摩擦块二4213受到的向左的力大于摩擦块二4213与摩擦块一4212之间的最大静摩擦力之前,膛压控制滑块4216的位置始终不变,出灰口424始终处于密封状态,由于尾气箱弹簧4224可压缩,尾气箱气压控制滑块4223向右移动挤压尾气箱弹簧4224并对出气口一4226进行密封,当尾气箱气压控制滑块4223不能移动时,炉灰箱42内的气压逐渐升高直至和保温组件1内气压相等,在复位弹簧433的作用下异形板432回复到原来的位置,尾气通过保温组件1流入到尾气箱4225中,由于尾气箱4225中的出气口一4226被密封,只有出气口二4227出气,尾气箱4225的进气速度高于出气速度,尾气箱4225的气压增大,并最终推动尾气箱气压控制滑块4223向左移动,使炉灰箱42中的气压进一步增大,膛压控制滑块4216受到的向左的压力进一步增大并超过摩擦块一4212与摩擦块二4213之间的最大静摩擦力,使摩擦块二4213克服与摩擦块一4212之间的摩擦力向左滑动,摩擦块一4212与摩擦块二4213之间的摩擦力由最大静摩擦力减小为滑动摩擦力,膛压控制滑块4216在炉灰箱42中气压的作用下快速向左移动,膛压弹簧一4214与膛压弹簧二4215被压缩,出灰口424被打开,在气压的作用下炉灰箱42中的灰尘被吹出,炉灰箱42中的气压减小,由于膛压弹簧二4215挤压摩擦块二4213,使摩擦块二4213与摩擦块一4212之间仍然有摩擦力,摩擦块二4213与摩擦块一4212之间的摩擦力和炉灰箱42中气体对膛压控制滑块4216的合力大于膛压弹簧一4214的弹力,膛压控制滑块4216保持静止,当炉灰箱42中气压与大气压相同时,灰尘不再被吹出,膛压弹簧一4214的弹力大于摩擦块二4213与摩擦块一4212之间的摩擦力,在膛压弹簧一4214的作用下膛压控制滑块4216克服摩擦力向右移动并与限位块二4217接触,再次密封出灰口424;当膛压控制滑块4216向左移动并解除对出灰口424的密封时,由于炉灰箱42内气压减小,在尾气箱弹簧4224弹力的作用下,尾气箱气压控制滑块4223向右移动解除对出气口一4226的密封;通过保温管12的尾气被清理灰尘后通过连接管13流入尾气箱4225中,最终经出气通道三53流入余热锅炉中进行余热回收;当锅炉检修时,通过拉杆口423和螺纹孔8可将膛压控制滑块4216向左拉动,出灰口424被打开,将抽风机与出灰口424连接并抽风,可将保温管12与炉灰箱42中的残留灰尘进行清理。In specific use, the air outlet channel 3 53 is connected to the waste heat boiler, and the high-temperature exhaust gas flows into the rear insulation pipe 12 from the air inlet 11, and then passes through the self-rotating solid-gas one-way separation device 2, the vertical wall ash cleaning device 3, the connecting pipe 13 and In the exhaust box 4225, when the high-temperature exhaust gas flows through the self-rotating solid-gas one-way separation device 2 through the thermal insulation assembly 1, the exhaust gas will drive the rotating fan 22 to rotate, and the rotating fan 22 drives the central shaft 23, the upper bracket 26, the lower bracket 27 and the dust removal board 28 does concentric rotation, because the rotating fan 22 is inclined on the central axis 23, when the gas flowing in the vertical direction encounters the rotating fan 22, it will generate a horizontal component force on the rotating fan 22, and push the rotating fan 22 to rotate, Since the action of the force is mutual, the rotating fan 22 will exert a horizontal reaction force on the gas, and the rotating fan 22 will push the dust to fly into the brush one 24 through the horizontal reaction force exerted on the gas, and the dust removal plate 28 and the rotating The fan 22 rotates concentrically and the dust removal plate 28 extends into the brush one 24. The
本发明适用性强,可应用于烧结机余热锅炉、三废混燃炉及吹风气余热锅炉、水泥窑余热锅炉、钢铁余热锅炉、危废余热锅炉、垃圾焚烧余热锅炉、焦化余热锅炉、有色金属冶炼余热锅炉、矿热炉行业余热锅炉、玻璃窑余热锅炉、干熄焦余热锅炉、碳素窑余热锅炉、燃气蒸汽轮机余热锅炉、炼钢余热锅炉等余热锅炉的预除尘,并且操作简单,直接将本发明与余热锅炉连接即可实现无动力自动除尘、自动排尘、自动清洁。The invention has strong applicability and can be applied to sintering machine waste heat boilers, three-waste mixed combustion furnaces and blowing air waste heat boilers, cement kiln waste heat boilers, iron and steel waste heat boilers, hazardous waste waste heat boilers, waste incineration waste heat boilers, coking waste heat boilers, non-ferrous metal smelting Pre-dust removal of waste heat boilers, waste heat boilers in the submerged arc furnace industry, glass kiln waste heat boilers, CDQ waste heat boilers, carbon kiln waste heat boilers, gas steam turbine waste heat boilers, steelmaking waste heat boilers and other waste heat boilers, and the operation is simple, directly The invention can realize automatic dust removal, automatic dust removal and automatic cleaning without power by being connected with the waste heat boiler.
尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, and substitutions can be made in these embodiments without departing from the principle and spirit of the invention and modifications, the scope of the present invention is defined by the appended claims and their equivalents.
以上对本发明及其实施方式进行了描述,这种描述没有限制性,附图中所示的也只是本发明的实施方之一,实际的结构并不局限于此。总而言之如果本领域的普通技术人员受其启示,在不脱离本发明创造宗旨的情况下,不经创造性的设计出与该技术方案相似的结构方式及实施例,均应属于本发明的保护范围。The present invention and its embodiments have been described above, and the description is not restrictive, and what is shown in the accompanying drawings is only one of the embodiments of the present invention, and the actual structure is not limited thereto. All in all, if those of ordinary skill in the art are inspired by it, and without departing from the purpose of the present invention, any structural modes and embodiments similar to this technical solution are designed without creativity, all should belong to the protection scope of the present invention.
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210880816.2A CN115069053B (en) | 2022-07-26 | 2022-07-26 | A kind of exhaust gas dust separation filter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210880816.2A CN115069053B (en) | 2022-07-26 | 2022-07-26 | A kind of exhaust gas dust separation filter |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115069053A true CN115069053A (en) | 2022-09-20 |
CN115069053B CN115069053B (en) | 2023-08-15 |
Family
ID=83242557
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210880816.2A Active CN115069053B (en) | 2022-07-26 | 2022-07-26 | A kind of exhaust gas dust separation filter |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115069053B (en) |
Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106964580A (en) * | 2016-01-13 | 2017-07-21 | 王佳伟 | One kind is based on aerodynamic rotating brushes dedusting mechanism and dust removal method |
CN207270980U (en) * | 2017-09-27 | 2018-04-27 | 广东宏绿环保实业有限公司 | A Boiler Tail Gas Dust Removal Equipment |
CN207371219U (en) * | 2017-09-26 | 2018-05-18 | 新疆兵团现代绿色氯碱化工工程研究中心(有限公司) | A kind of cyclone dust collector for recycling calcium carbide stove exhaust waste heat |
CN208366097U (en) * | 2018-06-06 | 2019-01-11 | 郴州联华耐火材料有限公司 | A kind of exhaust passage of refractory material kiln |
CN209809735U (en) * | 2019-03-07 | 2019-12-20 | 东南大学 | An industrial waste gas dust gas separation device |
JP6630943B1 (en) * | 2019-06-17 | 2020-01-15 | 广州瑩冲渦輪増圧器有限公司 | Kitchen exhaust gas low cost exhaust treatment system |
CN211963379U (en) * | 2019-12-31 | 2020-11-20 | 沈阳山水原环保科技有限公司 | A dedusting and whitening device for flue gas desulfurization outlet |
CN214319455U (en) * | 2021-01-25 | 2021-10-01 | 湖北润楚生物科技有限公司 | Cyclone dust removal device |
CN214486057U (en) * | 2021-03-25 | 2021-10-26 | 张玮 | Workshop exhaust gas purification device |
CN113654369A (en) * | 2021-09-17 | 2021-11-16 | 四川省兴欣钒科技有限公司 | A waste heat utilization device for a rotary kiln and a method of using the same |
CN113975899A (en) * | 2021-11-16 | 2022-01-28 | 杨志彬 | Chain grate-rotary kiln denitration system |
-
2022
- 2022-07-26 CN CN202210880816.2A patent/CN115069053B/en active Active
Patent Citations (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106964580A (en) * | 2016-01-13 | 2017-07-21 | 王佳伟 | One kind is based on aerodynamic rotating brushes dedusting mechanism and dust removal method |
CN207371219U (en) * | 2017-09-26 | 2018-05-18 | 新疆兵团现代绿色氯碱化工工程研究中心(有限公司) | A kind of cyclone dust collector for recycling calcium carbide stove exhaust waste heat |
CN207270980U (en) * | 2017-09-27 | 2018-04-27 | 广东宏绿环保实业有限公司 | A Boiler Tail Gas Dust Removal Equipment |
CN208366097U (en) * | 2018-06-06 | 2019-01-11 | 郴州联华耐火材料有限公司 | A kind of exhaust passage of refractory material kiln |
CN209809735U (en) * | 2019-03-07 | 2019-12-20 | 东南大学 | An industrial waste gas dust gas separation device |
JP6630943B1 (en) * | 2019-06-17 | 2020-01-15 | 广州瑩冲渦輪増圧器有限公司 | Kitchen exhaust gas low cost exhaust treatment system |
CN211963379U (en) * | 2019-12-31 | 2020-11-20 | 沈阳山水原环保科技有限公司 | A dedusting and whitening device for flue gas desulfurization outlet |
CN214319455U (en) * | 2021-01-25 | 2021-10-01 | 湖北润楚生物科技有限公司 | Cyclone dust removal device |
CN214486057U (en) * | 2021-03-25 | 2021-10-26 | 张玮 | Workshop exhaust gas purification device |
CN113654369A (en) * | 2021-09-17 | 2021-11-16 | 四川省兴欣钒科技有限公司 | A waste heat utilization device for a rotary kiln and a method of using the same |
CN113975899A (en) * | 2021-11-16 | 2022-01-28 | 杨志彬 | Chain grate-rotary kiln denitration system |
Also Published As
Publication number | Publication date |
---|---|
CN115069053B (en) | 2023-08-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN113606599A (en) | Industrial flue gas waste heat recycling system | |
CN109772046A (en) | A kind of heavy duty detergent sack cleaner with crushing function for coal chemical industry | |
CN104740969B (en) | A kind of boiling type granular bed filter deduster | |
CN112933770A (en) | Chamber-divided back-blowing ash removal device for bag type dust collector | |
CN115069053A (en) | Tail gas and dust separation filter | |
CN109163584B (en) | Straight channel flue gas heat exchanger | |
CN213965699U (en) | Filter element ash handling equipment | |
CN204745928U (en) | High -temperature gas dust remover | |
CN206355754U (en) | Conductivity ceramics film high-temp. corrosion resistant deduster | |
CN204353027U (en) | A kind of 75 tons of dry-quenching secondary dust cleaners | |
CN218076952U (en) | Electric arc furnace flue gas recovery filter equipment is used in fused brick production | |
CN113739587B (en) | Ferrosilicon ore flue gas waste heat treatment device based on heat exchange principle | |
CN209685892U (en) | A composite dust collector and copper bottom blowing smelting equipment | |
CN202993234U (en) | Automatic rotary furnace ash cleaning device | |
CN110057202B (en) | Non-stop submerged arc furnace flue gas microsilica powder recovery system | |
CN203899320U (en) | Encircling-type blowing soot cleaning device | |
CN202097041U (en) | Filler type cyclone dust extractor | |
CN202683001U (en) | Grading dedusting system | |
CN2106002U (en) | Chain net transmission type electric dust remover | |
CN107149831B (en) | A kind of industrial filter cartridge type cleaner | |
CN222151351U (en) | Dust removal control device for mold maintenance room | |
CN219756348U (en) | Wear-resistant hearth of circulating fluidized bed boiler | |
CN117839349B (en) | Wall flow type honeycomb ceramic high-temperature dust removing device | |
CN213221486U (en) | Cluster type spark catcher | |
CN211676785U (en) | Gas injection device for dust removing equipment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address | ||
CP03 | Change of name, title or address |
Address after: 221000 China Resources Industrial Park, Huaihai International Port District, Xuzhou City, Jiangsu Province Patentee after: Jiangsu Sifang Clean Energy Equipment Manufacturing Co.,Ltd. Address before: West Bianmin Road, China Resources Industrial Park, Xuzhou Huaihai International Port Area, Xuzhou City, Jiangsu Province 221142 Patentee before: JIANGSU SIFANG BOILER Co.,Ltd. |